CN109825336A - The recycling processing method of waste saccharide liquid in a kind of sucrose trichloride production process - Google Patents
The recycling processing method of waste saccharide liquid in a kind of sucrose trichloride production process Download PDFInfo
- Publication number
- CN109825336A CN109825336A CN201910149486.8A CN201910149486A CN109825336A CN 109825336 A CN109825336 A CN 109825336A CN 201910149486 A CN201910149486 A CN 201910149486A CN 109825336 A CN109825336 A CN 109825336A
- Authority
- CN
- China
- Prior art keywords
- saccharide liquid
- waste saccharide
- production process
- processing method
- waste
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Landscapes
- Processing Of Solid Wastes (AREA)
Abstract
The invention discloses a kind of recycling processing methods of waste saccharide liquid in sucrose trichloride production process, comprising the following steps: chooses waste saccharide liquid, lime or lime slurry is added, is handled at 60 DEG C~108 DEG C, obtains the suspension containing dechlorination organic matter.By the processed waste saccharide liquid of method provided by the present invention, it can be used as auxiliary fuel, auxiliary agent, it is used for example as the auxiliary material of fuel coal water slurry, the material of firing bricks with industrial wastes, achieve the effect that recycling while realizing the environmental protection treatment of waste saccharide liquid, it can offer reference for the environment protection treating of Sucralose enterprise, promote industry healthy development.
Description
Technical field
The invention belongs to changing rejected material to useful resource processing technology fields, and in particular to give up sugar in a kind of sucrose trichloride production process
The recycling processing method of liquid.
Background technique
Sucralose is the functional sweetener using sucrose as raw material, and in its production process, 1 ton of product of every acquisition is about
It can generate useless sugared (chlorinated sucrose and the chlorinated sucrose ester waste) of 1.5-3 tons of dry matter equivalents, the useless sugared dry matter heat of per kilogram
Value is about 4000 kilocalories.The stock solutions that the waste liquid or crystallization and purification that these useless sugar major parts are obtained with extraction and separation obtain are deposited
, therefore waste saccharide liquid caused by Sucralose per ton is produced up to 4-15 tons of waste saccharide liquids, CODcr is generally up to hundreds of thousands of millis
Gram per liter.Since waste saccharide liquid quantity is big, COD value is high, it is processed into for one in Sucralose environmental protection of enterprise control
Priority and difficulty problem, or even influence the sound development of Sucralose industry.
Since waste saccharide liquid has the feature of high cod values and its chlorine-bearing compound biodegrade hardly possible, waste saccharide liquid is diluted laggard
Row sewage treatment is unpractical.It is the more satisfactory approach of one kind (assuming that waste saccharide liquid CODcr by waste saccharide liquid progress burning disposal
It is 14KJ calculating by 1 gram of CODcr organic matter heat for 300,000 mg/L, then per kilogram waste saccharide liquid can produce 1000 kilocalorie heats, because
This can both realize environmental protection treatment using its heat generated by burning, and go back escapable cost).However since waste saccharide liquid high temperature fires
Releasably a large amount of chlorine, the hydrogen chloride further generated by chlorine can be to burning facility generation heavy corrosions, if do not located when burning
Reason can also bring secondary pollution problem, and the Chlorobenzens further generated by chlorine are then environmental carcinogen dioxin-like chemical
(PCDD/Fs) important precursor needs further to take measures to prevent and reduce the generation of dioxin-like chemical, or
The burning for taking measures to remove before flue gas emission, therefore directly carrying out waste saccharide liquid has high in burning facility and technical aspect
It is required that furthermore the chlorinated sucrose ester in waste saccharide liquid has low aqueous solubility and high-adhesiveness, difficulty is also brought along on burning conveying,
So directly carrying out burning disposal to waste saccharide liquid is being currently the problem of industry.
Summary of the invention
For the intractable status of waste saccharide liquid in above-mentioned sucrose trichloride production process, the purpose of the present invention is to provide one kind
The recycling processing method of waste saccharide liquid in sucrose trichloride production process, this method is simple, economic, at the environmental protection for realizing waste saccharide liquid
It can achieve the effect that recycling while reason.
Above-mentioned purpose of the invention can be achieved through the following technical solutions: give up sugar in a kind of sucrose trichloride production process
The recycling processing method of liquid, comprising the following steps: choose waste saccharide liquid, lime or lime slurry is added, carried out at 60~108 DEG C
Processing, obtains the suspension containing dechlorination organic matter.
In above-mentioned sucrose trichloride production process in the recycling processing method of waste saccharide liquid:
Preferably, the waste saccharide liquid includes at least one of water and chlorinated sucrose and chlorinated sucrose ester.
Preferably, the moisture content of the waste saccharide liquid is 55~95wt%.
Preferably, the lime includes at least one of calcium oxide and calcium hydroxide.
Preferably, the dosage of the lime is 5~45wt% of waste saccharide liquid gross mass.
Preferably, the lime slurry includes but is not limited to be reacted by calcium oxide with water, or add water by calcium hydroxide
It modulates, or is modulated by calcium oxide and calcium hydroxide mixing and water adding.
Preferably, the dosage of the lime slurry is calculated as 5~45wt% of waste saccharide liquid gross mass by dry hydrogen calcium oxide.
Preferably, it is handled 0.5~8 hour at 60~108 DEG C.
Preferably, the answering in terms of including but not limited to auxiliary fuel or auxiliary agent of the suspension containing dechlorination organic matter
With.
Preferably, auxiliary material or internal combustion of the suspension containing dechlorination organic matter in including but not limited to fuel coal water slurry
The application baked bricks in terms of material.
Basic principle of the invention is to generate hydrolysis using calcium hydroxide and waste saccharide liquid, and the sugar hydrolysis dechlorination that gives up generates de-
Chlorine organic matter and calcium chloride can when then waste saccharide liquid processed by the invention burns as auxiliary material since calcium chloride is non-combustible matter
It avoids effectively mitigating hydrogen chloride bring relevant issues, to achieve the purpose that waste resource recovery utilizes.
The present invention have it is following the utility model has the advantages that
(1) chlorinated sucrose, the chlorinated sucrose ester in waste saccharide liquid are carried out water using cheap raw material by the method for the present invention
Dechlorination is solved, is obtained by dechlorination organic matter, the mixed reactant of calcium chloride, calcium hydroxide and water composition, due to the generation of calcium chloride,
So that originally can with waste saccharide liquid burn and discharge chlorine be fixed, efficiently solve the problems, such as waste saccharide liquid for burning it is secondary；By
It is fixed in originally flammable chlorine, treated waste saccharide liquid recycling is used for auxiliary combustion as auxiliary material, raw material, both realizes
Being effectively treated for useless sugar, will not bring secondary pollution, and can produce certain economic benefit；Such as the auxiliary material as water-coal-slurry,
Dechlorination organic matter burning therein is generated compared with high heating value, can correspondingly save fuel, calcium chloride therein is conducive to water-coal-slurry
Dispersion and stablize, calcium hydroxide therein plays the role of adjusting water-coal-slurry pH, and can generate in combustion system fixation chlorine from
The harmful substances benefit such as son, sulfur dioxide uses water when water therein directly can replace preparing water-coal-slurry, can correspondingly reduce water
Dosage；
(2) the method for the present invention reaction condition is mild, easy to operate, can meet production needs well, be well suited for work
Industryization is used；
(3) the method for the present invention realizes the resource utilization of waste, turns waste into wealth, and makes economic benefit, environmental benefit and society
Meeting benefit brings out the best in each other, and can offer reference for the environment protection treating of Sucralose enterprise, promote industry healthy development.
Specific embodiment
Following embodiment is used merely to explain the present invention, and protection scope of the present invention is not intended to be limited to following implementation
Example.The those of ordinary skill of the technical field based on the contents of the disclosure of the present invention and the scope of each parameter, can be real
The existing purpose of the present invention.
Embodiment 1
Sucralose (content 99.3%) 350g is taken, 950g water is added to dissolve, obtains the Sucralose that moisture content is 73.1wt%
Solution is added 300g lime toward aqueous solution of sucrose trichloride under stiring, is stirred to react at 65 DEG C 5 hours.Every 30 in reaction process
Minute sampling filtering, filtrate acetic acid on the rocks neutralize, and measure Sucralose content with HPLC, the results are shown in Table 1.
Table 1 be added in aqueous solution of sucrose trichloride lime when being reacted for 65 DEG C Sucralose with the time content
Embodiment 2
Sucralose (content 99.5%) 350g is taken, 950g water is added to dissolve, obtains the Sucralose that moisture content is 73.1wt%
Solution is added 300g lime toward aqueous solution of sucrose trichloride under stiring, is stirred to react at 85 DEG C 3 hours.Every 30 in reaction process
Minute sampling filtering, filtrate acetic acid on the rocks neutralize, and measure Sucralose content with HPLC, the results are shown in Table 2.
Table 2 be added in aqueous solution of sucrose trichloride lime when being reacted for 85 DEG C Sucralose with the time content
| Reaction time | 0 minute | 30 minutes | 60 minutes | 90 minutes | 120 minutes | 150 minutes | 180 minutes |
| Sucralose (%) | 12.3 | 2.6 | 0.3 | 0.0 | 0.0 | 0.0 | 0.0 |
Embodiment 3
Sucralose (content 99.2%) 350g is taken, 950g water is added to dissolve, obtains the Sucralose that moisture content is 73.1wt%
Solution, is added 300g lime toward aqueous solution of sucrose trichloride under stiring, and stirring is warming up to feed liquid boiling (104 DEG C), insulation reaction 3
Hour.Every 30 minutes sampling filterings in reaction process, filtrate acetic acid on the rocks neutralize, and measure Sucralose content with HPLC, as a result
As shown in table 3.
Table 3 be added in aqueous solution of sucrose trichloride lime when being reacted for 104 DEG C Sucralose with the time content
| Reaction time | 0 minute | 30 minutes | 60 minutes | 90 minutes | 120 minutes | 150 minutes | 180 minutes |
| Sucralose (%) | 0.2 | 0.0 | 0.0 | 0.0 | 0.0 | 0.0 | 0.0 |
Comparative example 1
Example 3 adds 950g water to dissolve, obtaining moisture content is with batch Sucralose (content 99.2%) 350g
The sucralose solution of 73.1wt%.
Embodiment 4
The feed liquid of feed liquid and comparative example 1 after taking 1~3 reaction treatment of above-described embodiment is concentrated under reduced pressure respectively, is dry,
Number consecutively is A1, A2, A3, S1, carries out chlorine element analysis, the results are shown in Table 4.
Chlorine element analyzes result in 4 feed liquid of table
| Sample number into spectrum | Unit | Perchloro- | Chlorine in ash | Ash content | Flammable chlorine | Non-combustible chlorine |
| A1 | % | 8.73 | 18.63 | 42.73 | 0.77 | 7.96 |
| A2 | % | 8.56 | 20.05 | 41.80 | 0.18 | 8.38 |
| A3 | % | 8.64 | 22.84 | 37.70 | 0.02 | 8.62 |
| S1 | % | 22.73 | 0 | It is ashless | 22.73 | 0 |
Above-described embodiment is using Sucralose as the representative object of chlorinated sucrose in waste saccharide liquid ingredient, by detect feed liquid three
Chlorine cane sugar content can sufficiently react out-feed liquid in processes dechlorination the case where, chlorine element comparison (Examples 1 to 3 and comparison
Example 1 compares) analysis shows feed liquid fully can convert non-combustible chlorine for flammable chlorine by processing of the invention, further
Illustrate that by processing, dechlorination is may be implemented in feed liquid.
Embodiment 5
(moisture content is the waste saccharide liquid 2000g for taking trichloro-cane-6-ethyl ester purification section in sucrose trichloride production process to generate
75.36wt%), (water is the waste saccharide liquid 2000g generated with Sucralose treatment and finishing section in sucrose trichloride production process
75.72wt%), 450g lime is added under stiring, is warming up to 65 DEG C and reacts 8 hours.
Embodiment 6
The waste saccharide liquid 2000g that trichloro-cane-6-ethyl ester purification section generates in sucrose trichloride production process is taken, wherein useless sugar
Liquid moisture content is 79.55wt%, and 400g lime is added under stiring, is warming up to 90 DEG C and reacts 4 hours.
Embodiment 7
The waste saccharide liquid 4500g that Sucralose treatment and finishing section generates in sucrose trichloride production process is taken, wherein waste saccharide liquid contains
Water rate is 70.32wt%, is added under stiring by 1500 grams of lime slurries (conversion is that dry hydrogen calcium oxide weighs 750 grams), is warming up to
101 DEG C are reacted 1 hour.
Comparative example 2
Example 7 is concentrated under reduced pressure with batch waste saccharide liquid, is dry, and number S2 carries out chlorine element analysis and calorific value inspection
It surveys, is as a result summarized in table 5.
Embodiment 8
Feed liquid after taking 5~7 reaction treatment of above-described embodiment, is concentrated under reduced pressure respectively, is dried, number consecutively B1,
B2, B3 carry out chlorine element analysis and calorific value detection, are as a result summarized in table 5.
The analysis of 5 sample chlorine element of table and heating value test results
Embodiment 9
Treated the feed liquid of Example 6,7 separates and handles dechlorination organic matter dry product, number D1, D2, detection hair
Heat, testing result: D1 19373KJ/kg, D2 19584KJ/kg.
Explanation in relation to chlorine element analysis, calorific value detection in above-mentioned comparative example, embodiment:
(1) detection of chlorine is according to microcoulomb pond chlorine detector (GB/T 3558-1996) in chlorine element analysis, the inspection of ash content
It surveys according to thermogravimetry (GB/T 212-2008)；(2) perchloro-, flammable chlorine and non-combustible chlorine are with original sample for calculating base；(3) in ash
Chlorine is with ash for calculating base；(4) chlorine * ash content in non-combustible chlorine=ash；(5) the flammable non-combustible chlorine of chlorine=perchloro--；(6) calorific value
According to bomb method (GB/T 213-2008)；(7) calorific value is As-received testing result.
From 5~7 feed liquid of embodiment be concentrated under reduced pressure, be dried after sample and 2 sample chlorine element of comparative example analysis and fever
Testing result is measured, 8 organic matter heating value test results, available: (1) organic matter (chlorination sugarcane in waste saccharide liquid in conjunction with the embodiments
Sugar, chlorinated sucrose ester) chlorine that contains is flammable chlorine, it is released in combustion process；(2) the useless sugar handled through the method for the present invention
Dechlorination reaction has occurred in liquid, organic matter, and chlorine therein is converted into non-combustible chlorine by flammable chlorine, forms ash content in combustion；
(3) waste saccharide liquid processed by the invention, dechlorination organic matter calorific value increase.
To sum up, the waste saccharide liquid in sucrose trichloride production process is handled by the method for the present invention, can reach environmental protection treatment
It is required that and realizing the purpose of waste resource recovery.
Claims (10)
1. the recycling processing method of waste saccharide liquid in a kind of sucrose trichloride production process, it is characterized in that the following steps are included: choosing
Waste saccharide liquid is added lime or lime slurry, is handled at 60 DEG C~108 DEG C, obtain the suspension containing dechlorination organic matter.
2. the recycling processing method of waste saccharide liquid in sucrose trichloride production process according to claim 1, it is characterized in that: institute
Stating waste saccharide liquid includes at least one of water and chlorinated sucrose and chlorinated sucrose ester.
3. the recycling processing method of waste saccharide liquid in sucrose trichloride production process according to claim 2, it is characterized in that: institute
The water content for stating waste saccharide liquid is 55~95wt%.
4. the recycling processing method of waste saccharide liquid in sucrose trichloride production process according to claim 1, it is characterized in that: institute
Stating lime includes at least one of calcium oxide and calcium hydroxide.
5. the recycling processing method of waste saccharide liquid in sucrose trichloride production process according to claim 4, it is characterized in that: institute
The dosage for stating lime is 5~45wt% of waste saccharide liquid gross mass.
6. the recycling processing method of waste saccharide liquid in sucrose trichloride production process according to claim 1, it is characterized in that: institute
It states lime slurry and is reacted by calcium oxide with water, or add water to modulate by calcium hydroxide, or by calcium oxide and calcium hydroxide
Mixing and water adding is modulated.
7. the recycling processing method of waste saccharide liquid in sucrose trichloride production process according to claim 6, it is characterized in that: institute
The dosage for stating lime slurry is calculated as 5~45wt% of waste saccharide liquid gross mass by dry hydrogen calcium oxide.
8. the recycling processing method of waste saccharide liquid in sucrose trichloride production process according to claim 1, it is characterized in that:
60 DEG C~108 DEG C are handled 0.5~8 hour.
9. the recycling processing method of waste saccharide liquid in sucrose trichloride production process according to claim 1, it is characterized in that: institute
State application of the suspension containing dechlorination organic matter in terms of auxiliary fuel or auxiliary agent.
10. the recycling processing method of waste saccharide liquid in sucrose trichloride production process according to claim 1, it is characterized in that:
Application of the suspension containing dechlorination organic matter in terms of the auxiliary material of fuel coal water slurry or firing bricks with industrial wastes material.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910149486.8A CN109825336A (en) | 2019-02-28 | 2019-02-28 | The recycling processing method of waste saccharide liquid in a kind of sucrose trichloride production process |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910149486.8A CN109825336A (en) | 2019-02-28 | 2019-02-28 | The recycling processing method of waste saccharide liquid in a kind of sucrose trichloride production process |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN109825336A true CN109825336A (en) | 2019-05-31 |
Family
ID=66864834
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201910149486.8A Pending CN109825336A (en) | 2019-02-28 | 2019-02-28 | The recycling processing method of waste saccharide liquid in a kind of sucrose trichloride production process |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN109825336A (en) |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101460447A (en) * | 2006-05-23 | 2009-06-17 | V.B.医疗保险私人有限公司 | Recovery of dimethylformamide and other solvents from process streams of manufacture of trichlorogalactosucrose |
| US20130197215A1 (en) * | 2011-10-14 | 2013-08-01 | Lexington Pharmaceuticals Laboratories, Llc | Chlorination of Carbohydrates and Carbohydrate Derivatives |
| CN105764880A (en) * | 2013-11-27 | 2016-07-13 | 塔特和莱利技术有限公司 | Waste treatment process comprising treating waste stream with base at elevated temperature |
-
2019
- 2019-02-28 CN CN201910149486.8A patent/CN109825336A/en active Pending
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101460447A (en) * | 2006-05-23 | 2009-06-17 | V.B.医疗保险私人有限公司 | Recovery of dimethylformamide and other solvents from process streams of manufacture of trichlorogalactosucrose |
| US20130197215A1 (en) * | 2011-10-14 | 2013-08-01 | Lexington Pharmaceuticals Laboratories, Llc | Chlorination of Carbohydrates and Carbohydrate Derivatives |
| CN105764880A (en) * | 2013-11-27 | 2016-07-13 | 塔特和莱利技术有限公司 | Waste treatment process comprising treating waste stream with base at elevated temperature |
Non-Patent Citations (2)
| Title |
|---|
| C.B.阿杰尔松: "《石油化工工艺学》", 31 December 1990, 中国石化出版社 * |
| 中国科协学会部编: "《中国科学技术协会第四届优秀建议奖获奖项目汇编》", 31 August 2001, 中国科协学会部出版 * |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN102234170B (en) | Method and device for rapidly reducing moisture content of sludge | |
| CN106588386B (en) | Harmless treatment method for antibiotic fermentation residues for manufacturing organic fertilizer | |
| Li et al. | Hydrothermal treatment coupled with pyrolysis and calcination for stabilization of electroplating sludge: Speciation transformation and environmental risk of heavy metals | |
| Gu et al. | Co-pyrolysis of sewage sludge and Ca (H2PO4) 2: heavy metal stabilization, mechanism, and toxic leaching | |
| CN115283424B (en) | A method for co-processing fly ash from incineration of medical waste and fly ash from incineration of domestic garbage | |
| CN110937772A (en) | Method for separating organic/inorganic components from sludge | |
| Han et al. | Roles of dehydration conditioners on the formation of apatite phosphorus during the pyrolysis of various sludge | |
| CN107363074B (en) | A kind of aluminium cell carbonaceous materials recycling is the method for alternative fire coal | |
| CN112128779A (en) | Incineration treatment method for high-chlorine-content hazardous waste | |
| Melgaço et al. | Phosphorus recovery from liquid digestate by chemical precipitation using low‐cost ion sources | |
| CN103506372B (en) | Coal-fired furnace slag processing method | |
| CN109825336A (en) | The recycling processing method of waste saccharide liquid in a kind of sucrose trichloride production process | |
| CN108410505A (en) | A method of preparing water-gas using organic dangerous waste | |
| Fang et al. | Preparation of phosphorus containing products by co-incineration of sludge ash and calcium-based additives: Focusing one-step and multi-step method | |
| CN217121223U (en) | Resourceful treatment system of industry waste salt | |
| Pöykiö et al. | The use of a sequential leaching procedure for assessing the heavy metal leachability in lime waste from the lime kiln at a caustizicing process of a pulp mill | |
| Pan et al. | Distribution and transformation behaviors of heavy metals during liquefaction process of sewage sludge in ethanol-water mixed solvents | |
| CN104893784B (en) | Waste of polymeric containing cyanogen as cement plant alternative fuel processing method | |
| CN110395834A (en) | The processing method of the waste water of the doctorization containing organochlorine | |
| CN111112286A (en) | Organic waste treatment method | |
| CN105110353A (en) | Method for carbonizing by-product soda solution used for water treatment by using micro-silicon powder as raw material | |
| CN112794868B (en) | Method for treating sodium tetrachloroaluminate generated in methyl dichlorophosphine production process | |
| CN104694166A (en) | Graded pyrolysis gasifying system and application thereof, and treatment method of leather-producing wastes | |
| CN105368495A (en) | Method for preparing synthesis gas from organic dissolvant and biomass residue | |
| JP7465322B1 (en) | Method for producing modified incineration ash, and modified incineration ash |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| RJ01 | Rejection of invention patent application after publication | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20190531 |